Technical Field
[0001] The present invention relates to a yeast for fermenting a saccharified solution in
bioethanol production using lignocellulosic biomass.
[0002] In particular, the present invention relates to a yeast capable of effectively producing
ethanol from pentose (which may be, hereinafter, also referred to as C5) and hexose
(which may be, hereinafter, also referred to as C6) in bioethanol production using
lignocellulosic biomass.
Background Art
[0003] Bioethanol is expected to be a renewable resource that is produced by biomass. Moreover,
since carbon dioxide that is produced by combustion of bioethanol is carbon neutral,
increased use of bioethanol is considered to suppress increase of carbon dioxide,
which is a main cause of the global warming.
[0004] Bioethanol is obtained by fermenting biomass and distilling and purifying ethanol.
It is necessary to produce much alcohol from saccharified solutions for increasing
the yield of bioethanol. Since the yeasts generally used in the process of bioethanol
production cannot convert pentose such as xylose and arabinose into alcohol, only
hexose has been used as raw materials for fermentation.
[0005] Typical biomass is reported to contain 35-45% of cellulose, 25-40% of hemicellulose,
and 15-30% of lignin, though the contents vary according to raw materials. Therefore,
use of hemicellulose, which mainly contains the pentose xylose, but not only cellulose,
which is a polymer of hexose, as a substrate should lead to effective ethanol production.
[0006] Xylose is reported to be the second abundant sugar in biomass next to glucose and
it is an important object in bioethanol production to use pentose effectively.
[0007] Techniques for using xylose, even at a little amount, by imparting the ability to
utilize xylose by genetic recombination, using microorganism that produces ethanol
from xylose, or the like have been so far disclosed.
[0008] Patent Literature 1 discloses an invention involving converting xylose (C5) into
xylulose by introducing a gene having the xylose transporter activity into a host
cell to incorporate it in the pentose phosphate pathway of the glycolysis and use
it for fermentation.
[0009] Patent Literature 2 discloses a technique for producing alcohol with yeast provided
with an arabinose transporter. This involves incorporation of arabinose (C5) via arabitol
and xylulose in the pentose phosphate pathway in the glycolysis to use it for fermentation,
similar to the invention of Patent Literature 1.
[0010] Non-Patent Literature 1 discloses provision of xylose utilization ability by incorporating
a xylose utilization gene derived from Escherichia coli in Zymomonas.
[0011] Non-Patent Literature 2 describes production of ethanol from xylose by yeast in the
genus Pichia.
Citation List
Patent Literature
Non Patent Literature
[0013]
Non Patent Literature 1: Zhang, M., et al., Science, 1995. Vol. 267, pp. 240-243.
Non Patent Literature 2: Bicho, P.A., et al., Appl. Environ. Microbiol., 1988, Vol. 54, pp. 50-54.
Summary of Invention
Technical Problem
[0014] However, the invention of Patent Literature 1 involves introducing a protein having
the xylose transporter activity derived from Candida guilliermondii into Saccharomyces
cerevisiae as a host. Accordingly, a foreign gene would be introduced.
[0015] The invention of Patent Literature 2 is also an invention involving introduction
of a gene from a species different from the host, although the transporter gene is
different.
[0016] The technique described in Non-Patent Literature 1 also involves introduction of
a xylose utilization gene. The technical concept thereof is different from Patent
Literature 1 and 2 described above, but they are similar in that a foreign gene is
introduced.
[0017] Therefore, any of the invention described in Patent Literature 1 and 2 and Non-Patent
Literature 1 requires adopting a containment measure to comply with "the Cartagena
Protocol on Biosafety to the Convention on Biological Diversity" adopted in the United
Nations. Accordingly, they require facilities for ensuring the biosafety and therefore
it is disadvantageous in cost to produce ethanol using such yeasts.
[0018] Moreover, use of yeast in the genus Pichia by the technique described in Non-Patent
Literature 2 does not result in a much higher efficiency of ethanol production because
the low xylose availability in the wild-type Pichia yeast.
[0019] An object of the present invention is to obtain a fermentative yeast having a highly
efficient ethanol production without introducing a foreign gene.
Solution to Problem
[0020] The present invention features a fermentative yeast that effectively produces ethanol
from pentose and hexose and is deposited to NITE Patent Microorganisms Depositary
(NITE Patent Microorganisms Depositary, National Institute of Technology and Evaluation
(Independent Administrative Institution), #122, 2-5-8 Kazusakamatari, Kisarazu-shi,
Chiba 292-0818, Japan) on November 19, 2014 (accession date) under the accession number
NITE BP-01964 (hereinafter, also referred to as strain BP-01964).
[0021] The wild-type Meyerozyma guilliermondii has a xylose utilization ability. However,
it does not have sufficient ability to utilize xylose for the bioethanol production.
The strain BP-01964 was obtained by the strain improvement of Meyerozyma guilliermondii
and selection of yeasts that utilize pentose at a high efficiency. As a result, a
yeast comprising ethanol productivity about twice as high as that of the parental
strain was selected.
[0022] Moreover, the present invention features introduction of a self-cloned transaldolase,
alcohol dehydrogenase, pyruvate decarboxylase, xylose reductase, xylitol dehydrogenase,
transketolase, or formate dehydrogenase into the aforementioned Meyerozyma guilliermondii
strain.
[0023] The introduction of an enzyme gene from Meyerozyma guilliermondii itself does not
necessitate any containment measure to comply with the Cartagena Act. Therefore, conventional
facilities can be used without needing special facilities for biosafety.
Brief Description of Drawings
[0024]
FIG. 1 illustrates the amounts of ethanol production in the strain BP-01964 and the
parent strain (the strain N).
FIG. 2 illustrates glucose and xylose utilization abilities in slurry fermentation.
FIG. 3 illustrates yields of fermentation in slurry fermentation and in clear liquid
fermentation.
FIG. 4 illustrates the ethanol production ability of the strain BP-01964 with a corn
stover clear liquid.
Description of Embodiments
[0025] The ascomycete yeast Meyerozyma guilliermondii comprises the xylose utilization ability.
A yeast of the accession number NITE BP-01964 was obtained using the strain N of Meyerozyma
guilliermondii as the parent strain by the breeding involving selection of mutants
with mutagenesis.
[0026] In general, mutagenesis involves use of irradiation of ultraviolet rays or radioactive
rays, alkylating agents such as N-ethyl-N-nitrosourea (ENU) and ethyl methanesulfonate
(EMS), base analogs such as BrdU, or nitroso compounds such as nitroamine or nitrosoguanidine.
In the present invention, mutagenesis was carried out by irradiation of UV or addition
of a chemical such as EMS.
[0027] Methods for obtaining yeast strains are described below.
Examples
1. Isolation of yeast strain
[0028] The parent strain of Meyerozyma guilliermondii was cultured with a sugar solution
derived from rice straw. Rice straw from Kumagaya, Japan was immersed in an equal
amount of a 25% ammonium solution at 80°C for 3 hours and then ammonia was allowed
to be evaporated. The pH of the treated biomass was adjusted to 4 with 10% NaOH and
then Acremonium cellulase (manufactured by Meiji Seika Pharma Co., Ltd.) was added
to conduct enzymatic saccharification at 50°C for 72 hours. The solid-liquid separation
of the produced slurry was conducted by filter-pressing to collect the liquid. Using
this liquid (hereinafter, also referred to as clear liquid), habituation in culture
was conducted with addition of a mutagen for 19 months and strains with improved fermentation
performance were selected. The selection was based on the amount of ethanol after
a certain time period. A strain with high fermentation performance was deposited to
NITE Patent Microorganisms Depositary, National Institute of Technology and Evaluation
(Independent Administrative Institution) under the accession number NITE BP-01964.
2. Properties of the strain
2.1 Ethanol production ability
[0029] FIG. 1 illustrates the amount of ethanol production in the strain BP-01964 in comparison
with that of the strain N, the parent strain. Corn stover was treated with dilute
sulphuric acid and the resultant saccharified liquid whose pH was adjusted to 6 with
an NaOH aqueous solution was used. A liquid culture of the strain was added so that
the OD
600 of the medium became 2.0 and the resultant liquid culture was cultured at 30°C for
96 hours. The amount of ethanol after the culturing is illustrated. Glucose in the
saccharified solution was 63.2 g/L and xylose was 34.5 g/L. Ethanol was measured using
GC-FID (manufactured by GL Sciences Inc.: GC390B).
[0030] As seen in FIG. 1, the obtained strain produces ethanol more than 2 times as much
as the wild type does. Since the obtained strain has an improved ethanol production
relative to the wild type strain, the obtained strain is considered to have an improved
ability to utilize xylose, which is C5. Therefore, the glucose and xylose utilization
abilities of the strain were examined.
[0031] Next, rice straw was treated with an ammonium aqueous solution in a similar way to
the ammonia treatment described above and then Acremonium cellulase was added to conduct
enzymatic saccharification at 50°C for 72 hours. Fermentation was conducted using
the produced slurry.
[0032] The slurry fermenter has a jacket structure and the temperature was regulated by
the circulation of warm water through the jacket part. Air ports are provided at the
bottom and fermentation was conducted with continuously providing a predetermined
amount of filtered air through the air ports at the bottom with agitation with impellers
coupled with a motor.
[0033] The change over time in amount of glucose, xylose, and ethanol contained in the slurry
was analyzed. Glucose and xylose were measured by sampling and centrifuging the slurry
and measuring the resultant supernatant by HPLC. Ethanol was measured using GC-FID
(manufactured by GL Sciences Inc.: GC390B) as described above. The result is shown
in FIG. 2.
[0034] Glucose, which is C6, is consumed earlier, but as glucose in the slurry decreases,
xylose, which is C5, is consumed to produce ethanol. Since the obtained yeast comprises
both C5 and C6 utilization abilities, it can produce ethanol efficiently. Therefore,
it is a strain that is also useful in industrial production.
2.2 Slurry fermentation ability, clear liquid fermentation ability
[0035] A yeast that efficiently carries out fermentation both with slurry and with clear
liquid in the bioethanol production is preferred. Therefore, the fermentation yields
with slurry and with clear liquid were compared. The fermentation yield is calculated
by the following equation.

[0036] As illustrated in FIG. 3, the obtained strain can exhibit equivalent performance
both in slurry fermentation and in clear liquid fermentation.
2.3 Ethanol production ability with corn stover sugar liquid
[0037] Like rice straw, corn stover is biomass often used for bioethanol production. The
obtained strain efficiently produces bioethanol with corn stover as well, although
it is a strain isolated by conducting habituation with a clear liquid produced from
rice straw.
[0038] Corn stover from Iowa, the United States, was immersed into 2 times volume of 3.7%
by weight sulfuric acid aqueous solution and treated at 170°C for 10 minutes. After
transfer to normal temperature, pH of the solution was adjusted to pH 4 with a 4 M
sodium hydroxide aqueous solution and an enzyme for biomass saccharification (such
as Acremonium cellulase, manufactured by Meiji Seika Pharma Co., Ltd.) was added to
conduct enzymatic saccharification at 50°C for 72 hours. The solid-liquid separation
of the produced slurry was conducted by centrifugation to collect the liquid (hereinafter,
referred to as corn stover clear liquid).
[0039] Fermentation with a corn stover clear liquid whose pH was adjusted to pH 6 with an
NaOH aqueous solution was conducted with the obtained strain and the amount of ethanol
production was measured over time. The result is shown in FIG. 4. While the ethanol
production of the wild type (the strain N) reaches a plateau after 48 hours, the obtained
strain continues producing ethanol until 72 hours later and can produce ethanol at
a final yield that is about 1.5 times as high as that of the wild type.
[0040] Moreover, transaldolase, which is an enzyme in the pentose phosphate pathway, alcohol
dehydrogenase, which is an enzyme that produces ethanol from acetaldehyde, or pyruvate
decarboxylase, which produces acetaldehyde, which is a substrate of alcohol dehydrogenase
from pyruvic acid, can be genetically introduced into the strain obtained in the present
invention to further facilitate use of xylose.
[0041] For example, the following procedures can be adopted for the genetic introduction.
Amplify the gene to be introduced and a terminator region thereof (hereinafter, referred
to as gene + terminator region) by PCR. Amplify a promoter region to be used for the
introduction. These should be both amplified by PCR from the chromosomes of the strain
of Meyerozyma guilliermondii used in the present invention.
[0042] Clone the DNA fragments amplified by PCR into a commercially available vector for
Escherichia coli by infusion in the order of promoter, gene + terminator region. Transform
Escherichia coli with the cloned vector and amplify the vector. Obtain DNA fragments
for homologous recombination by cutting out the promoter and gene + terminator region
from the amplified vector with restriction enzymes or amplifying the promoter and
gene + terminator region from the amplified vector by PCR.
[0043] Homologous recombination of the strain with the obtained DNA fragments was performed
to obtain a desired strain. Electroporation was used for the homologous recombination.
Genetic introduction in this manner allows introduction of multiple copies into the
chromosomes and therefore enhancement of the activity of the introduced enzyme.
[0044] As a DNA fragment for the homologous recombination, for example, the promoter of
xylose reductase, transaldolase + terminator may be preferably used because transaldolase
is considered to work efficiently when using the promoter of xylose reductase that
functions in the xylose utilization.
[0045] Specifically, the xylose reductase promoter is amplified with the following primers
of SEQ ID NO: 1 and SEQ ID NO: 2 and the transaldolase gene and the terminator region
were amplified with the following primers of SEQ ID NOs: 3 and 4.
SEQ ID NO: 1: AAGGCTTGGGAACTTTCTTT
SEQ ID NO: 2: AGCAATTGATGATTAATTTT
SEQ ID NO: 3: ATGACCAATTCTCTTGAACA
SEQ ID NO: 4: AAATTGTGCCGTGTCAAACT
[0046] Moreover, the promoter of GAPDH and alcohol dehydrogenase + terminator may be preferably
used. Since the GAPDH is a strong promoter that functions in glycolysis, it is considered
to be an efficient promoter for use as a promoter of alcohol dehydrogenase, which
is an enzyme in glycolysis. Alcohol dehydrogenase produces NAD
+ when it is NADH-dependent as well as serves to convert acetaldehyde into ethanol.
Therefore, it serves to enhance the effect of NAD
+-dependent xylitol dehydrogenase.
[0047] Specifically, the GAPDH promoter is amplified with the primers of the following SEQ
ID NO: 5 and SEQ ID NO: 6 and the alcohol dehydrogenase gene and terminator region
is amplified with the primers of the following SEQ ID NOs: 7 and 8.
SEQ ID NO: 5: GTTGTAGCGGAGGCTCAATT
SEQ ID NO: 6: TGTATAATTTAAATGTGGGT
SEQ ID NO: 7: ATGTCAATTCCAGAATCCAT
SEQ ID NO: 8: CACCTTGGCTGGAAGTGCTG
[0048] Furthermore, besides transaldolase and alcohol dehydrogenase, enzymes such as pyruvate
decarboxylase, xylose reductase, xylitol dehydrogenase, transketolase, and formate
dehydrogenase may be cloned in the down stream of any of the aforementioned promoters
and introduced into the obtained strain to confer resistance to organic acids such
as acetic acid, aldehyde such as furfural, and the like, which are present when a
sugar solution is produced.
[0049] Pyruvate decarboxylase, xylose reductase, xylitol dehydrogenase, transketolase, and
formate dehydrogenase can be amplified with the following primers.
Pyruvate decarboxylase
[0050]
SEQ ID NO: 9: ATGACAGAAATTACTTTGGG
SEQ ID NO: 10: ACAAACAAATGCTGAAAAC
Xylose reductase (XR)
[0051]
SEQ ID NO: 11: ATGTCTATTACTTTGAACTC
SEQ ID NO: 12: CACAAAAGTTGGAATCTTGT
Xylitol dehydrogenase (XDH)
[0052]
SEQ ID: NO 13: ATGACTCCCAACCCATCTTT
SEQ ID NO: 14: CTCGGGACCATCTATAATAA
Transketolase (TLK)
[0053]
SEQ ID NO: 15: ATGACCACCGACGACTACGA
SEQ ID NO: 16: AACAGCTAGCAAGTCCTGA
Formate dehydrogenase (FDH)
[0054]
SEQ ID NO: 17: ATGAGTCCAGCAACAAAAGG
SEQ ID NO: 18: TTTCATCTTGTGTCTTTCAC
[0055] Moreover, while the strains obtained by this method comprise an introduced gene,
they belong to a category to be treated as a non-modified yeast under the Cartagena
Act because it is self-cloned.